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Environ. Eng. Res. 2019
Review Article https://doi.org/10.4491/eer.2018.134 pISSN 1226-1025 eISSN 2005-968X In Press, Uncorrected Proof
Petroleum sludge treatment and disposal: A review Olufemi Adebayo Johnson1†, Augustine Chioma Affam2
1School of Energy, Geoscience, Infrastructure and Society, Heriot-Watt University Malaysia, No. 1, Jalan Venna P5/2, Precinct 5, 62200 Putrajaya, Malaysia 2Civil Engineering Department, University College of Technology Sarawak, Persiaran Brooke, 96000 Sibu, Sarawak, Malaysia
Abstract Petroleum industry produces one of the popular hazardous waste known as Petroleum Sludge. The treatment and disposal of petroleum sludge has created a major challenge in recent years. This review provides insights into various approaches involved in the treatment, and disposal of petroleum sludge. Various methods used in the treatment and disposal of petroleum sludge such as Incineration, stabilization/solidification, oxidation, and bio-degradation are explained fully and other techniques utilized in oil recovery from petroleum sludge such as solvent extraction, centrifugation, surfactant EOR, freeze/thaw, pyrolysis, microwave irradiation, electro-kinetic method, ultrasonic irradiation and froth flotation were discussed. The pros and cons of these methods were critically considered and a recommendation for economically useful alternatives to disposal of this unfriendly material was presented. Keywords: Hazardous waste, Petroleum sludge, Sludge disposal, Waste management
This is an Open Access article distributed under the terms of the Creative Commons Attribution Non-Commercial Li- cense (http://creativecommons.org/licenses/by-nc/3.0/)
which permits unrestricted non-commercial use, distribution, and repro- duction in any medium, provided the original work is properly cited.
Received April 4, 2018 Accepted August 7, 2018 † Corresponding Author E-mail: [email protected] Tel: +60-173847589 Fax: +60-3-8894-3999
ORCID: 0000-0003-0745-880X
Copyright © 2019 Korean Society of Environmental Engineers http://eeer.org
1. Introduction
In the production and exploration of petroleum, wastes are generated which includes drilling
fluid, petroleum wastewater, petroleum effluent treatment plant sludge and bottom tank sludge.
A petroleum refinery with a production capability of 105,000 drums per day make approximately
50 tons of oily sludge per year [1]. The remains found at the base of tank and other storage
facilities are generally refered to as sludge. For crude oil storage vessels, this kind of sludge
found at its base comprises of hydrocarbons, asphaltenes, paraffin, water, and inorganic solids
such as sand, iron sulfides and iron oxides. Hydrocarbon is the principal component of petroleum
sludge, which is formed when crude oil’s properties are changed as a result of changes in
external conditions. The formation of petroleum sludge are commonly caused by cooling below
the cloud point, evaporation of light ends, mixing with incompatible materials, and the
introduction of water to form emulsions [2].
According to Resources Conservation and Recovery Act (RCRA) sludge is separated as a
hazardous waste, alongside other hazardous wastes [3]. The elemental composition of petroleum
sludge is Nitrogen, Phosphorous, Potassium, Iron, Copper, Calcium, Magnesium, Cadmium,
Phosphate, Chromium, Zinc, Sodium, and Lead [4].
Crude oily sludge is a recurrent problem leading to corrosive effects and a reduction in oil
storing capacity. The economic effect includes the cost of sludge removal and disposal, where
the greater expense is the disposal fee of the environmentally-unfriendly material.
An assortment of methods for processing and disposing of petroleum sludge is used globally,
including: thermal, mechanical, biological, and chemical. Altogether, these are not economically
sustainable. In summation to the cost of removing, transferring, and land filling involved in
cleaning up the petroleum sludge, the sludge also contains several toxic compounds. These
contaminants include petroleum hydrocarbons, such as aliphatic hydrocarbons and polycyclic
aromatic hydrocarbons (PAHs); over 33% of total petroleum hydrocarbons (TPH) with 550
mg/kg of PAHs are present in petroleum oily sludge [5], polychlorinated biphenyls (PCBs), and
heavy metals, including barium, lead, zinc, mercury, chromium, arsenic, and nickel [6-8].
Producers, refiners and transporters of petroleum materials should take congnisance of the
removal of tank sludge as a very important maintainance practice.
Every storage tanks will accumulate sludge over-time, but petroleum storage tank poses a
bigger problems at production locations. Beneficial reuse of petroleum sludge from small
production locations necessitates that the sludge material be reused without treatment. The use of
this waste as a construction material, should prove very economical and environmentally
sustainable.
2. Petroleum Sludge
Petroleum sludge compositions contain both organic components and heavy metals with typical
range of concentrations as reported by the American petroleum institute (API) [9]. According to
more recent research works, high concentration of metals in petroleum sludge from refineries was
reported as Zn (1,299 mg/kg), Fe (60,200 mg/kg), Cu (500 mg/kg), Cr (480 mg/kg), Ni (480
mg/kg), and Pb (565 mg/kg) [10-13].
The improper disposal of petroleum sludge to the environment, create a major threat such as
significant modifications in the chemical and physical properties of the surrounding soils,
resulting in morphological change [14]. Deficiency in nutrient and stunted growth in the
vegetation of receiving soils have been described [15]. The sludge’s high viscosity fixes it in soil
pores and results in a continuous envelope of the airfoil of the land [16]. Reduction in
hygroscopic moisture, hydraulic conductivity, and wetting power of soils have been described in
the presence of petroleum sludge [16, 17]. Elements of high molecular weight have been observed
to form hydrophobic crusts thus reducing the availability of water and water-air exchange into the
soil [18]. Its long-term effect on farming land have been reported in western Canada [14].
Ineffective treatment and improper disposal of petroleum into the environment is of a major
health concern, it contains petroleum hydrocarbons (PHCs) and PAHs that are genotoxic to
humans and animals [14]. The PHCs can infiltrate the soil profile into the groundwater, causing a
grave menace to the aquatic systems [16, 19]. The presence of PHCs in the soil decreases the
diversity of soil microorganisms [17]. The petroleum sludge composition includes a heavy
concentrate of PHCs and PAHs. Most of these components are recalcitrant because of their tight
molecular bonds, heavy molecular weight, hydrophobicity and little solubility in water.
Proper management of petroleum waste has received greater attention due to increased
production and hazardous nature. Several approaches have been prepared to manage it with the
aim of bringing down the hazardous contaminant concentration or rendering them motionless, and
then as to relieve the environmental and health impact of the unfriendly material. These
approaches include, but are not restricted to, the following; landfarming/landfilling,
photocatalysis, incineration, solidification/stabilization, solvent extraction, ultrasonic treatment,
pyrolysis, chemical handling, and biodegradation [19-24]. Regarding the nature of the hazardous
waste, environmental policies and the cost of treatment, but a few of the aforementioned
approaches have been successful. Some of the methods employed in recycling hydrocarbons from
petroleum sludge are: solvent extraction, centrifugation treatment, surfactant enhanced oil
recovery (EOR), frost and melt treatment, sludge pyrolysis, microwave radiation, electromagnetic
method, ultrasonic radiation, and froth flotation.
In most of the treatment methods, three phases of waste management technique are used [25],
there are (1) reduction of petroleum sludge production through the use of technologies, (2) oil
recovery from the oily sludge, and (3) disposal of the unrecoverable petroleum sludge [26, 27].
Stage one helps prevent and reduce petroleum sludge generation, while the other two phases focus
on the effective treatment of crude oily sludge.
In this segment we shall survey some of the available treatment techniques and oil recovery
methods of petroleum sludge, their advantages and disadvantages will be spotlighted. Various
methods utilized in the disposal of petroleum sludge involved Incineration,
stabilization/solidification, oxidation, and biodegradation will also be discussed [28].
2.1. Oil Recovery from Petroleum Sludge
Equally one of the 3 Rs of sustainability, recycling has proven to be one of the major alternatives
to manage petroleum sludge. Recycle is the reprocessing and reformulation of oily sludge with
high concentration of oil (> 50%) and a relatively low concentration of solids (< 30%) by the
petroleum industry for energy recovery. Recycling will positively reduce the volume of
hazardous petroleum sludge from storage tanks, and therfore preventing environmental pollution
and reducing the economic consumption of non-renewable energy resources. In the USA, eighty
percent (80%) of PHCs sludge generated at the refinery are recycled, while the other 20% was
effectively done through approved disposal method [29].
2.1.1. Solvent extraction
This is the procedure by which solvent is used at desired proportions to remove non-volatile and
semi-volatile organic compounds from ground or water matrices, the oil is separated from the
solvent through a distillation process of the mixture [30].
Gazinou et al. [31] investigated the use of turpentine as a solvent for the extraction of
petroleum from petroleum sludge, they establish that the recovered oil amounts to about 13-53%
of the initial sludge quantity. Zubaidy and Abouelnasr [22] investigated the impact of methyl
ethyl ketone (MEK) and liquefied petroleum gas condensate (LPGC) as an extraction solvent. The
outcome indicates that the high oil recovery rate of 39% can be obtained using MEK while 32%
can be achieved using LPGC at Solvent-to-Sludge ratio of 4:1. Recovered oil by MEK exhibit an
improved ash, carbon residue and asphatene levels, though higher levels of sulfur and carbon
residue thus requires purification before use.
El Naggar et al. [32] compare different solvents by measuring their extraction effects on
dry/semi dry petroleum sludge. Among the solvents tested were naphtha cut, n-heptane, kerosene
cut, methylene dichloride, ethylene dichloride, toluene, and diethyl. The results show toluene as
the solvent with the highest recovery rate of about seventy-five percent (75.94%). Morealso
Meyer et al. [33] establish that petroleum solvent containing a considerable amount of ring
compounds is most effective in dissolving asphaltenic components in petroleum sludge.
Hexane and xylene have also been proven to be an effective recovery, solvent of hydrocarbons
from petroleum sludge, recovering up to 67.5% of PHCs in sludge, mostly in the range of c9 to c25
[34].
Various solvents has been used by different researchers for oily sludge and as reported by El
Naggar et al. [32] toluene solvent has proved to be the best and more effective for oily sludge
treatment with the highest recovery rate. In summary, solvent extraction is a simple, efficient
method of extraction that can be carried out in a short period. Nevertheless, when used in a large
scale extraction, low efficiency and high variability was reported [35]. It will be necessary to
develop some alternative methods to complement solvent extraction in order to improve its
performance.
2.1.2. Centrifugation treatment
In this method a pre-treated petroleum sludge is drawn through a high-speed rotating equipment
with strong centrifugal forces to break up its elements according to their different densities in a
short duration. Pre-treatment of the oily sludge is done to reduce it viscosity and thus enhance
centrifugation performance and save energy. Some of the pre-treatment method includes the
addition of agents such as organic solvents, demulsifying agents and tension active chemicals, the
injection of steam, and direct heating [22, 36-38]. Cambiella et al. [37] found that the water-oil
separation efficiency of centrifugation can be improved up to 92-96% with the gain of a modest
quantity of a coagulant salt.
Centrifugation treatment process involves mixing the pre-treatment agents with the oily sludge
and the mixture is treated in a pre-treatment tank in order to reduce the viscosity. During the
centrifugation process the water is separated from the oil (though still containing water and
solids), the separated water will be further treated for PHCs removal, while the oil will also be
separated from the solids and water to recover the oil using gravimetric separator. All the
separated water and solids are further treated in accordance to the environmental standards.
Centrifugation is an advanced clean and efficient method for petroleum sludge treatment. It does
not require high energy consumption,. However, it requires large space for the installation of the
plant, it is very costly and pose environmental concern (noise and pollution) [26, 39].
2.1.3. Surfactant enhanced oil recovery (EOR)
This is the process of removing organic pollutants from solid media in a cost effective and fast
way, through the application of surfactant. Surfactants are amphiphilic compounds containing
both hydrophobic groups as "tails" and hydrophilic groups as "head". It has the ability to lower
surface tension or interfacial tension between different types of liquids and between liquids and
solids, thus enhance its application in removal of organic pollutants [40]. Example of surfactants
that can increase the PHCs concentrations in aqueous phases includes, sodium dodecyi sulphate
(SDS), corexit 9527, Triton X-100, Tween 80 and Afonic 1412-7 [41-44].
Abdel-Azim et al. [45] and Dantas et al. [46] investigated the application of three different types
of surfactant based on nonyl phenol ethoxylates (n = 9, 11, 13) prepared for study. These were
composed of 4% inorganic acid solution, 10% of aqueous phase solution composed of NP-9, NP-
11 and NP-13 as surfactants and isopropyl or butyl alcohol as co-surfactants and the balance of
the system was an oil phase (benzene/toluene, 1:1 mixture). The phase separation period for the
mixture was 6 h and results showed that more than 80% water can effectively be removed from
the sludge. The effect of demulsifier system composition and its concentration in parts per
million were observed and was found that the best for complete breakdown of the sludge was the
one based on NP-13.
The application of chemical surfactants is fast and cost effective, however, there exist concerns
due to environmental toxicity and resistance to biodegradation. Though in the recent times
attention has been given to the development of biosurfactant that are more environmentally
friendly and biodegradable [41, 47-55].
2.1.4. Freezing and thawing treatment
Demulsification is one major method of oil recovery from petroleum sludge, whereby the water is
separated from the oil. Freeze/thaw treatment was employed as an effective demulsification
process for petroleum sludge in cold regions [56-58].
Freezing and thawing treatment involve two mechanisms for effective demulsification. The first
mechanism is when the water phase in the mixture freezes ahead the oil, volume expansion of
frozen water droplets result in the coalescence of the water, leading to internal disarrangement of
the mixture and then the oil gradually freezes with decrease in temperature. The interfacial
tension causes the oil phase to coalesce during the thawing phase resulting in separation of the
mixture of oil and water in different phases by gravitational force [59]. In the second mechanism
the oil frozen before the water results in the development of a solid cage, thus capturing water
droplets during the freezing process. The captured water droplets froze as the temperatures drop
thus increasing in volume, the increased volume forces open the oil cage, creating a mixed phase
of oil and water that can be separated by gravitational force [59].
Jean et al. [60] discovered that the freeze/ thaw process can generate over 50% of oil from
refinery oil-water mixture, whilst Chen and He [56] found that 90% of water can be separated
from a high water content petroleum sludge.
More than 90% of water were successfully separated from the lubricating oily sludge with
application of freezing and thawing method [61]. Lin et al. [58] investigated the effect of four
different freezing methods (freezing in a refrigerator, cryogenic bath, dry ice and liquid nitrogen),
it was discovered that freezing in cryogenic or dry ice show the best performance of over 70%
dehydration efficiency of a mixture containing 60% water.
Application of this method will be very well suited for cold regions where natural freezing is
possible, though it has its limitation with respect to temperature, duration, water content, salinity
of the aqueous phase, presence of surfactant, and solid contents [58].
2.1.5. Sludge pyrolysis
The thermal decomposition of organic materials at high temperatures (500-1,000°C) in an inert
environment is called pyrolysis. Hydrocarbons with lower molecular weights are produced
during pyrolysis either in condensation (liquid) or non-condensable gases. The end product is
always char, liquid, and gases depending on procedural conditions [62, 63]. It was discovered
that pyrolysis of oily sludge leads to an increase in oil yield at increased temperature to an
optimum temperature of 525°C, and at a further heating above 525°C sees a decrease due to
secondary composition as expressed by Shen and Zhang [64]. 80% of total organic carbon in
Petroleum sludge can be converted into usable hydrocarbons using a range of 327-450°C
pyrolysis as discovered by Liu et al [20]. The proficient separation of oil from sludge happens at
460 to 650°C with about 70 to 80% of the oil separated as revealed by Schmidt and Kaminsky
[65]. However the maximum output rate of hydrocarbons is at 440°C as revealed by Chang et al
[66]. Pyrolysis of oily sludge starts at a low temperature of 200°C while at 350 to 500°C, the
production of maximum hydrocarbon is achieved with improved oil production as revealed by
Wang et al. [67].
Pyrolysis process produces products in fluid phase, making storage and transportation of the
recovered oil easy. The recovered oil was also found to share similar qualities and properties with
low-grade petroleum distillates from refineries and can be used directly to fuel diesel engines [68,
69]. However, pyrolysis can be limited by various factors, such as temperature, heating rate,
characteristics of the sludge and chemical additives. Furthermore, it is not cost effective [70-72],
and the product may contain high concentrations of PAHs [73].
2.1.6. Microwave irradiation
This process involves the application of microwave frequency in an industrial scale ranging from
900-2,450 MHz [74]. The microwave energy is applied to oily sludge through molecular
interaction with the electromagnetic field, resulting in rapid, efficient heating compared with the
conventional methods. The heating caused demulsification of the mixture of oil and water, by
increasing the temperature of the oil/water mixture thus reducing the viscosity and accelerating
the water droplets settlement in the mixtures [75]. The dense hydrocarbons can also be broken by
the rapid temperature increase into lighter hydrocarbons. In oily sludge the inner phase is water
and it can absorb more microwave energy than oil. The energy absorption in the inner phase of
the oil/water mixture results in the expansion of water thus reducing the interfacial film between
the water and oil, which could facilitate the separation. The optimum microwave irradiation
power and treatment time were 420 W and 12 s, respectively.
In one investigation, the application of microwave irradiation on 188 barrels of water-oil
emulsion gave 146 barrels of oil and 42 barrels of water, with a higher separation efficiency
compared to conventional method [76].
Microwave irradiation performance can be limited by factors such as, microwave power,
microwave duration, surfactant, pH, salt and some properties of the sludge [77]. Compared to
other techniques that involves heating, microwave irradiation can rapily raise the energy of
molecules within the medium resulting in higher reaction rates within a very short period of time,
which make the method a high energy-efficient. However,it application at industrial-scale is
limited because of equipment requirement and high operating cost.
2.1.7. Electrokinetic method
This is the process of using direct current (DC) of low-intensity across a pair of electrodes on a
permeable medium, resulting in the movement of electron from the lower concentration region to
the higher concentration region through the permeable medium in the liquid phase. The respective
electrode also enjoy an exchange charged particles of ions and electrophoresis in a colloidal
system [78, 79].
Application of electrokinetic method in separation of petroleum sludge is always a three stage
mechanism. The first is the breaking down of the colloidal aggregates in the presence of an
electrical field that causes migration of colloidal particles of the sludge and solid phase to the
anode area (electrophoresis) and the migration of the separated liquid phase in the cathode area
(electro-osmosis) [79].
Elektorowicz and Habibi [80] applied electrokinetics in the treatment of oily sludge, the results
show that the water content of the sludge can be removed by 63% and light hydrocarbon by 43%,
50% of light hydrocarbon was removed when electrokinetic was combined with surfactant.
Though effective, the performance of electrokinetic method can be reduced through various
factors such as pH, electrical potential, resistance, and spacing of the electrodes. The application
of electrokinetic process for oil recovery from oily sludge compared to other recovery methods
such as centrifugation and pyrolysis requires less amount of energy. However, the electrokinetic
process studies on oily sludge recovery has only been carried out at the laboratory level, and the
performance and cost at a large scale still need further investigation.
2.1.8. Ultrasonic irradiation
In this process ultrasonic waves are used to generate compression and rarefactions in the
treatment chamber. Ultrasonic irradiation is an effective treatment method of separating solid-
liquid in high-concentration suspensions, by decreasing the stability of water-oil mixture [81-84].
During the ultrasonic irradiation process, ultrasonic wave propagates in the treatment medium
generates compressions and rarefactions, the compression cycle exerts a positive pressure on the
medium by pushing molecules together, while the rarefaction cycle exerts a negative pressures by
pulling molecules from each other. The negative pressure thus generate microbubbles, which
when grows to an unstable level collapsed violently and cause a shock waves resulting in very
high temperature and pressure. The cavitation leads to an increased temperature of the emulsion
system and decreased in its viscosity thus enhances mass transfer of the liquid phase, resulting in
the destabilization of water-oil mixture [85]. Ultrasonic irradiation is more effective compared to
other methods in the sense that it can clean both the solid particle surface and also penetrates into
different regions of a multiphase system [86].
Xu et al. [19] investigated the use of ultrasonic cavitation with a frequency of 28 kHz in oil
recovery operation of oily sludge in an ultrasonic cleaning tank; oil separation rate of 55.6% was
reported. They also reported that optimum temperature, acoustic pressure, and the ultrasonic
power to be; 40°C, 0.10 MPa, and 28 kHz, respectively, and that all these factors can affect the oil
recovery operation. Zhang et al. [87] found that 80% oil recovery rate can be achieved from oily
sludge-water mixtures within 10 min using ultrasonic irradiation with 20 kHz frequency at a
power of 66 W.
Ultrasonic treatment is a highly efficient method without environmental pollution (green
treatment), that can be carried out in a very short time. However, factors which include, treatment
duration, frequency, water content in the mixture, temperature, solid particle size, initial PHCs
concentration, sonication power & intensity, salinity, and presence of surfactant can limit its
performance and it is also very costly method [83, 88, 89].
2.1.9. Froth flotation
In this technique, the oil droplets/small solids capturing process is achieved through the use of air
bubbles in aqueous slurry, the oil droplets/small solids are then floated and collected in a froth
layer [90]. In this process, a sludge slurry need to be formed, by adding specified amount of water
to the oily sludge. Air is injected to form fine bubbles that meet the oil droplets in the sludge
slurry, the decrease and rupture of the water film between the oil droplets and air bubble allows
the oil droplets to migrate toward air bubbles, then the mixture of air bubbles and the oil droplets
float to the water surface where the accumulated oil can be collected separately for further
purification [91].
Ramaswamy et al. [92] found that oil recovery of up to 55% can be achieved through the
application of froth flotation for the treatment of oily sludge at optimum flotation conditions.
Al-Otoon et al. [93] used, modified fluidized flotation process to recover bitumen from sand
tar, with 0.35 Wt% of an extraction solvent; 86 Wt% of the bitumen was recovered. Stasiuk et al.
[94] reported that the surfactant addition in the froth flotation process significantly decreases the
water content (10 v/v %) in the oil recovered.
Though effective, froth floatation process can be affected by oily sludge properties (viscosity,
solid content, and density), pH, salinity, temperature, air bubble size, presence of surfactant, and
treatment duration [95-97].
3. Petroleum Sludge Disposal Methods
Disposal methods are applied to petroleum sludge following oil recovery of all useful oil and
hydrocarbons. Among various methods used are: incineration, oxidation, solidification
/stabilization, and biodegradation.
3.1. Incineration
This is the process by which waste sludge from the petroleum industry undergoes complete
combustion in the presence of abundant air and auxiliary fuel. Two major incinerator types used
are rotary kiln and fluidized bed. Combustion temperatures in rotary kiln incinerators range
between 980-1,200°C, with a residence time of 30 min, while combustion temperatures in the
fluidized bed range between 730-760°C, with a residence time measured in days [98]. Fluidized
bed is best in treatment of sludge with low-quality because of it has high mixing efficiency, fuel
flexibility, low pollutant emissions and high combustion efficiency [99].
Sankaran et al. [100] found out that when three types of oily sludge were treated using a
fluidized bed incinerator without auxiliary fuels, a high combustion efficiency of 98-99% was
obtained, though the sludge with high content of water must be pre-treated to reduce their
viscosity before feeding in the incinerator.
3.2. Stabilization/Solidification
Solidification/stabilization (S/S) is a process of encapsulating/ sealing of waste using a binder
with the sole aim of preventing the waste leaching into the environment, whether through physical
or chemical means and to be able to convert the products to eco-friendly construction materials or
non-hazardous waste in the disposal landfill. The S/S of hazardous waste by cements involves
three major stages:
I. Correcting the chemical contaminants – which involve the chemical interactions between
the hydration products of the cement and the contaminants itself.
II. Physically absorbing the contaminants present on the surface of hydrated products of the
cements.
III. The encapsulation of contaminated waste or soil (low permeability of the hardened pastes)
[101, 102].
In the first and second stages above, it is of most importance to take good note of the nature of
the hydration products and the contaminants, because they determine the results while the third
stage depends on what sort of hydration products and nature of the pore structure characteristics
of the paste. S/S has been globally used in the treatment before disposal of most hazardous waste,
low-level radioactive and mixed wastes, as well as remediation of contaminated sites. According
to the US Environmental Protection Agency (USEPA), S/S is best Demonstrated Available
Technology (BDAT) for 57 hazardous wastes [103]. Of all the binders, hydraulic cements are the
most widely used for S/S of wastes. The end product can be used for construction purposes
depending on the characteristics.
Though S/S is fast and less costly compared to other disposal treatment methods, the release of
high concentration organic pollutant is possible when exposed to environmental leachants.
Karamaalidis and Voudrias [104] found that in S/S of refinery oily sludge, increased the cement
content lead to higher concentration of PAHs and TPH in the leachates.
In the process of improving the ineffectiveness of S/S in completely immobilizing the
hazardous contaminants, other materials are introduced into the mix. Caldwell et al used activated
carbon with Portland cement in the S/S treatment or management of organic contaminants and the
result showed a significant improvement [105]. Though activated carbon is however costly; a
possible cheap material that could combine sorption and binding characteristics is high carbon
power plant fly ash (HCFA), a pozzolanic material [106] similar to the PFA widely accepted for
use in cement-based construction materials [107], but which contains a higher proportion of
unburnt carbon. This carbon may act as a sorbent for organic compounds. Portland cement is
often used as a source of alkalinity and calcium to activate pozzolanic reactions in fly ash.
Leonard and Stegemann [108] investigated S/S of waste generated during petroleum
exploration and production using Portland cement (CEM1) with incorporation of HCFA as a
sorbent for organic contaminants, the result showed that the introduction of HCFA significantly
lowered the leaching of PHCs.
In S/S treatment of oily sludge the samples were prepared using concrete moulds sealed in
plastic bags to prevent possible carbonation due to exposure to air and cured for 24 h in a
humidity chamber with a relative humidity of 98 ± 2% and a temperature of 21 ± 3°C before
demoulding samples were resealed in plastic bags and transferred back into the humidity chamber
for further curing for 7, 28 and 56 d prior to testing [108].
Asna et al. [109] reported that the introduction of rice husk ash (RHA) at 5, 10, and 15% as
cement substitute material for solidify and stabilize the contaminant of oily sludge as an
alternative to reduce the toxicity before final disposal increased the compressive strength of the
product from 19.2 N/mm² to 24.9 N/mm².
3.3. Oxidation Treatment
Oxidation treatment is a degradation process of organic contaminants using chemical and other
oxidation agents. In oxidation process reactive agents are introduced into the oily sludge and the
organic compound in the oily sludge will be oxidized to carbon dioxide and water or into non-
hazardous materials [110]. Various oxidation reagent has been used in this process for oily sludge
treatment such as Fenton’s reagent, hypochlorite, ozone, ultrasonic irradiation, permanganate, and
persulfate. The application of Ultrasonic irradiation on the oily sludge oxidation process has also
proven to be effective. During the ultrasonication process which involves the application of sound
energy to agitate particles in the oily sludge sample intermediate radicals such as hydrogen (H*),
hydroxyl (OH*), hydroperoxyl (HO2*) and hydrogen peroxide (H2O2) will be produced which
enhance the breaking down of the complex hydrocarbons into simple hydrocarbons with high
solubility.
Mater et al. [21] discovered through their work that a Fenton type reagent can reduce the
concentration of PAHs, phenols, and other contaminants in oily sludge contaminated soil at a low
pH of 3.0. Zhang et al. [111] reported that the Fenton oxidation effect on oily sludge degradation
could be enhanced by ultrasonic irradiation.
Cui et al. [112] employed supercritical water oxidation (SCWO) method in the treatment of oily
sludge; they found that 92% of chemical oxygen demand (COD) were removed within 10 min
into the treatment. They also used wet air oxidation (WAO) in the treatment of oily sludge to
effectively remove 88.4% of COD within 9 min at temperature of 330°C with O2 excess of 0.8,
and this can be improved to 99.7% COD removal by adding a catalyst.
Oxidation treatment process can be done within a reasonably short period of time on oily sludge,
and it can be environmentally friendly (e.g., pollutant loading, temperature change, and the
presence of biotoxic substances, etc.) and the end products are biodegradable. However, for large
scale application, large amount of chemical reagents may be required, large equipment, increase
in energy consumption and invariable high cost of operation.
3.4. Bioremediation
The use of microorganisms in the biodegradation and removal of environmental pollutants has
been applied to land treatment, bio pile/composting and bio-slurry [113].
3.4.1. Land farming
Land farming treatment is a biological, chemical, and physical degradation of oily sludge
contaminants by mixing it with soil. Land treatment is more preferable to other disposal methods
because of its low cost, low energy consumption, has potential to accommodate large volumes of
sludge, and require simple operating procedure [114]. However, it is time consuming and requires
a very large area of land; it may not be effective in cold regions.
Marin et al. [115] reported that land farming treatment of oily sludge can remove 80% of
PHCs within 11 months of treatment in a semi-arid climate, the removal of half of the oily sludge
occurred within the first three months.
According to Admon et al. [13] reported that 70-90% of PHCs degradation can be achieved
within 2 months when land farming treatment was applied to oily sludge; it was observed that
most of the degradation occurs within the first 3 weeks of treatment.
Oily sludge land treatment for 12 mon under arid condition was investigated by Hejazi and
Husain [116], they observed that tilling (addition of water and nutrients) were the main
parameters responsible for the highest PHCs removal in land treatment of oily sludge with a
removal rate of 76%.
3.4.2. Bio pile/composting
The treatment method whereby petroleum wastes are turned into piles meant for degradation
through indigenous or extraneous micro-organisms is known as Bio pile. This treatment
technology can replace land treatment which requires large areas of land. This technology is
called composting when organic materials are added to improve its efficiency [12].
Wang et al. [117] reported that addition of bulking agent cotton stalk can significantly
improve the metabolic microbial activity when composting is employed in the treatment of oily
sludge. Liu et al. [118] reported that when manure is added to oily sludge during composting, the
microbial activity and diversity increase significantly.
Bio-augmentation using crude manure and straw was found to reduce the TPH content by 46-
53% during the composting of oily sludge within 56 days in the piles whilst 31% reduction rate
was recorded for control piles [119].
Kriipsalu et al. [120] stated that kitchen waste compost is the most efficient organic material
compared to sand amendment, matured oil compost, and shredded waste wood in the reduction of
TPH in oily sludge.
Biopile/composting treatment is environmentally friendly and requires less land space
compared to landing farming; however, large area of land is still needed and is also consume
more time.
3.4.3. Bio-slurry treatment
This method of treatment involves the mixture of sludge-associated solids and water (5-50% w/v),
the contaminants is dissolved into the aqueous phase where solubilized pollutants will be obtained
in large quantity. Microbial degradation of the pollutants will reduce the toxicity or turn the end
product into carbon dioxide and water.
Ayotamuwo et al. [121] reported that a TPH reduction of 40.7-53.2% can achieved within two
weeks and 63.7-85.5% can be achieved within six weeks in the application of bio-slurry treatment
for oily sludge. Ward et al [122] found that up to 80-99% TPH reduction can be obtained within
10-20 d of oily sludge biodegradation when bio-surfactant was added. Bio-slurry treatment is an
effective and fast disposal method for oily sludge and it only requires a small land area, however,
it is costly compared to other disposal technologies.
4. Conclusions
In the petroleum industry, the generation of oily sludge can not be avoided and this is pose a
global challenege in it treatment and management because of it hazardous nature. Several
approaches had evolved to effectively manage petroleum sludge, such as; pyrolysis, land farming,
ultrasonic treatment, Incineration, S/S, solvent extraction, photo catalysis, chemical treatment
and biodegradation. Table 1 presents the comparisons between various method of treatment and
disposal as discussed in this paper, considering the application stage, efficiency, advantages and
disadvantages. Some methods are very good in oil recovery but aare associated with high cost of
operation and their application at jarge scale may be limited., while others such as landfarming
are very simple in application with low cost of operation. However, it will take a very long time
(averagely 2 y) to have a complete treatment of the oily sludge and may also require a large land
area.
Table 1. Comparison of Treatment and Disposal Methods of Oily Sludge
Treatment Method Application
level
Average
oil
recovery
rate (%)
Advantages Disadvantages References
Solvent extraction Field 70 Simple,
efficient, and
save time
For large scale
extraction, low
efficiency and
high
variability
[22, 30-
35]
Centrifugation Field < 50 Clean and
efficient, does
not require
Large space
for the
installation of
[22, 26,
36-39]
high energy
consumption
the plant, it is
very costly
and pose
environmental
concern
Surfactant EOR Field 80 Fast and cost
effective
Environmental
toxicity and
resistance to
biodegradation
[40-55]
Freeze/thaw Laboratory 60 Suitable for
cold regions
Temperature,
duration, high
energy
consumption
[56-61]
Pyrolysis Field 70 Easy and
simple
High energy
consumption,
high
maintenance
and operating
cost
[20, 62-
73]
Microwave irradiation Field 90 Fast and
efficient
High energy
consumption,
high
maintenance
and operating
cost
[74-77]
Electrokinetic Laboratory 60 Fast and
efficient
Complicated
application and
only in small
scale
[78-80]
Ultrasonic irradiation Laboratory 70 Fast, highly
efficient
method
Very costly [19, 81-89]
without
environmental
pollution
Froth flotation Laboratory 60 Simple
application and
low energy
consumption
Low efficiency [90-97]
Incineration Field 90 Fast and
efficient
High cost of
equipment and
environmental
pollution
[98-100]
Stabilization/solidification Laboratory 90 Fast and
efficient
Only for oily
sludge with low
moisture
content(or dry
state) and the
end product
need proper
management
[101-109]
Oxidation Laboratory 90 Fast and
efficient
High cost of
operation,
environmental
pollution
[21, 110-
112]
Land farming Field 80 Low cost of
operation and
support large
scale treatment
Slow process,
require a very
large portion of
land and can
pose
environmental
concerns
[13, 114-
116]
Biopile/composting Field 80 Large capacity,
fast treatment
than land
High cost of
operation and
require land
[12,117-
120]
treatment area
Bioslurry Field 90 Fast treatment
and require
small land area
High cost of
operation and
proper
management of
the end product
[121, 122]
Since the problems of oily sludge generation is on increase, and most of the treatment
methods are quite costly or not effective; ultrasonic treatment, solvent extraction, incineration,
and S/S are costly, incineration is also linked with air pollution, whilst land farming and
degradation are not effective and associated with leaching of heavy metals, large field of land
and time eating up. The selection of the best treatment method may be based various elements
such as oily sludge composition, method capacity, costs, and available disposal standard. As
such, it may require special decision analysis approaches, to be able to evaluate the overall
performance of treatment methods presented in this paper. In the face of all the above stated cons
of the treatment and disposal of petroleum sludge, it is imperative to develop a more greener and
economically viable method to safely dispose this environmentally unfriendly materials.
In conclusion, as the dependency on petroleum products is increasing, which in turn
unavoidably lead to increased in the generation of petroleum sludge, it will be indispensable to
develop an economically useful alternative to the conventional disposal of petroleum sludge
without violating the environment and health safety. Through the development of an innovative
disposal approaches and new application of petroleum sludge, its disposal problem can be
overcome.
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